CA2389638C - Echangeur de reformage a faible perte de pression - Google Patents
Echangeur de reformage a faible perte de pression Download PDFInfo
- Publication number
- CA2389638C CA2389638C CA2389638A CA2389638A CA2389638C CA 2389638 C CA2389638 C CA 2389638C CA 2389638 A CA2389638 A CA 2389638A CA 2389638 A CA2389638 A CA 2389638A CA 2389638 C CA2389638 C CA 2389638C
- Authority
- CA
- Canada
- Prior art keywords
- catalyst
- tubes
- monolithic structures
- tube
- inside diameter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0292—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds with stationary packing material in the bed, e.g. bricks, wire rings, baffles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/30—Loose or shaped packing elements, e.g. Raschig rings or Berl saddles, for pouring into the apparatus for mass or heat transfer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
- C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
- C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
- C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/382—Processes with two or more reaction steps, of which at least one is catalytic, e.g. steam reforming and partial oxidation
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
- C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
- C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
- C01B3/34—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/384—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air by reaction of hydrocarbons with gasifying agents using catalysts with external heating of the catalyst
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00212—Plates; Jackets; Cylinders
- B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00309—Controlling the temperature by indirect heat exchange with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00477—Controlling the temperature by thermal insulation means
- B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/302—Basic shape of the elements
- B01J2219/30223—Cylinder
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/302—Basic shape of the elements
- B01J2219/30242—Star
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/322—Basic shape of the elements
- B01J2219/32296—Honeycombs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/55—Cylinders or rings
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0838—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel
- C01B2203/0844—Methods of heating the process for making hydrogen or synthesis gas by heat exchange with exothermic reactions, other than by combustion of fuel the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/14—Details of the flowsheet
- C01B2203/141—At least two reforming, decomposition or partial oxidation steps in parallel
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/14—Details of the flowsheet
- C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
- C01B2203/82—Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Méthode de production de gaz de synthèse et échangeur de reformage. La méthode comprend les étapes suivantes : le passage d'une première partie du mélange de charge d'hydrocarbures avec de la vapeur et d'un oxydant dans une zone de reformage catalytique autothermique à la vapeur pour former un premier gaz reformé à teneur réduite en hydrocarbures; le passage d'une deuxième partie du mélange de charge d'hydrocarbures avec de la vapeur dans une zone de reformage catalytique endothermique à la vapeur pour former un deuxième gaz reformé à teneur réduite en hydrocarbures; le mélange du premier et du deuxième gaz reformés ainsi que le passage du mélange formé dans une zone d'échange thermique pour qu'il soit refroidi, fournissant ainsi de la chaleur à la zone de reformage catalytique endothermique à la vapeur. La zone de reformage catalytique endothermique à la vapeur et la zone d'échange thermique sont placées respectivement du côté des tubes et du côté de la calandre d'un échangeur de reformage à calandre. L'échangeur de reformage comprend plusieurs tubes et des structures monolithiques porteuses de catalyseur à faible chute de pression. Le diamètre intérieur des tubes est inférieur à quatre fois la dimension maximale du bord des structures catalytiques.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/908,307 | 2001-07-18 | ||
| US09/908,307 US6855272B2 (en) | 2001-07-18 | 2001-07-18 | Low pressure drop reforming exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2389638A1 CA2389638A1 (fr) | 2003-01-18 |
| CA2389638C true CA2389638C (fr) | 2010-12-14 |
Family
ID=25425562
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2389638A Expired - Lifetime CA2389638C (fr) | 2001-07-18 | 2002-06-06 | Echangeur de reformage a faible perte de pression |
Country Status (10)
| Country | Link |
|---|---|
| US (2) | US6855272B2 (fr) |
| EP (1) | EP1277698B1 (fr) |
| KR (1) | KR100695052B1 (fr) |
| CN (1) | CN100448949C (fr) |
| AT (1) | ATE341525T1 (fr) |
| CA (1) | CA2389638C (fr) |
| DE (1) | DE60215080T2 (fr) |
| ES (1) | ES2269566T3 (fr) |
| MX (1) | MXPA02006987A (fr) |
| NO (1) | NO20023422L (fr) |
Families Citing this family (46)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6855272B2 (en) * | 2001-07-18 | 2005-02-15 | Kellogg Brown & Root, Inc. | Low pressure drop reforming exchanger |
| US6936238B2 (en) * | 2002-09-06 | 2005-08-30 | General Motors Corporation | Compact partial oxidation/steam reactor with integrated air preheater, fuel and water vaporizer |
| EP1413547A1 (fr) * | 2002-09-26 | 2004-04-28 | Haldor Topsoe A/S | Procédé pour la production de gas de synthèse |
| DE60336444D1 (de) * | 2002-09-26 | 2011-05-05 | Haldor Topsoe As | Verfahren zur Herstellung von Synthesegas |
| US8273139B2 (en) | 2003-03-16 | 2012-09-25 | Kellogg Brown & Root Llc | Catalytic partial oxidation reforming |
| US7138001B2 (en) * | 2003-03-16 | 2006-11-21 | Kellogg Brown & Root Llc | Partial oxidation reformer-reforming exchanger arrangement for hydrogen production |
| US7932296B2 (en) | 2003-03-16 | 2011-04-26 | Kellogg Brown & Root Llc | Catalytic partial oxidation reforming for syngas processing and products made therefrom |
| RU2343109C2 (ru) * | 2003-03-18 | 2009-01-10 | КЕЛЛОГГ БРАУН ЭНД РУТ ЭлЭлСи | Способ получения потока, обогащенного водородом, способ генерирования электрического тока, способ гидроочистки, устройство для получения потока, обогащенного водородом |
| AU2004238820B2 (en) | 2003-05-07 | 2008-01-31 | Shell Internationale Research Maatschappij B.V. | Silver-containing catalysts, the manufacture of such silver containing catalysts, and the use thereof |
| CA2524865A1 (fr) * | 2003-05-07 | 2004-11-25 | Shell Internationale Research Maatschappij B.V. | Systeme et procede de reacteur pour la fabrication d'oxyde d'ethylene |
| US20040224841A1 (en) | 2003-05-07 | 2004-11-11 | Marek Matusz | Silver-containing catalysts, the manufacture of such silver-containing catalysts, and the use thereof |
| US20040225138A1 (en) * | 2003-05-07 | 2004-11-11 | Mcallister Paul Michael | Reactor system and process for the manufacture of ethylene oxide |
| DE10359205B4 (de) * | 2003-12-17 | 2007-09-06 | Webasto Ag | Reformer und Verfahren zum Umsetzen von Brennstoff und Oxidationsmittel zu Reformat |
| US20050142049A1 (en) * | 2003-12-31 | 2005-06-30 | Amsden Jeffrey M. | Multi-tubular reactors with monolithic catalysts |
| TW200600190A (en) | 2004-04-01 | 2006-01-01 | Shell Int Research | Process for preparing a silver catalyst, the catalyst, and use thereof in olefin oxidation |
| JP2008514405A (ja) | 2004-09-24 | 2008-05-08 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | 成形粒子を選択するプロセス、システムを取り付けるプロセス、このようなシステム内で気体原料を反応させるプロセス、コンピュータプログラム製品、およびコンピュータシステム |
| WO2006045746A1 (fr) * | 2004-10-20 | 2006-05-04 | Shell Internationale Research Maatschappij B.V. | Procede de preparation d'un melange de monoxyde de carbone et d'hydrogene |
| EP1650160A1 (fr) * | 2004-10-20 | 2006-04-26 | Stichting Energieonderzoek Centrum Nederland | Procédé et réacteur pour la production de gaz de synthèse |
| WO2006045457A1 (fr) * | 2004-10-26 | 2006-05-04 | Haldor Topsøe A/S | Reacteur et procede de realisation de reactions catalytiques endothermiques ou exothermiques |
| US20070299148A1 (en) * | 2004-11-12 | 2007-12-27 | Verbist Guy Lode M M | Tubular Reactor With Packing |
| GB0507269D0 (en) * | 2005-04-11 | 2005-05-18 | Johnson Matthey Plc | Steam reforming |
| US7293533B2 (en) * | 2005-08-08 | 2007-11-13 | Utilization Technology Development, Nfp | Recuperative reforming reactor |
| KR100674864B1 (ko) * | 2005-09-29 | 2007-01-29 | 삼성전기주식회사 | 열특성이 우수한 연료 전지용 개질기 |
| US7207323B1 (en) | 2006-01-06 | 2007-04-24 | Utilization Technology Development, Nfp | Catalytic core reactor for thermochemical heat recovery |
| DE102006033441B4 (de) * | 2006-06-29 | 2009-05-07 | Enerday Gmbh | Reformer für ein Brennstoffzellensystem |
| US20080016768A1 (en) | 2006-07-18 | 2008-01-24 | Togna Keith A | Chemically-modified mixed fuels, methods of production and used thereof |
| US7635456B2 (en) * | 2006-08-08 | 2009-12-22 | Kellogg Brown & Root Llc | Low pressure drop reforming reactor |
| US7501078B2 (en) | 2007-01-10 | 2009-03-10 | Air Products And Chemicals, Inc. | Process for generating synthesis gas using catalyzed structured packing |
| US7887764B2 (en) * | 2007-09-18 | 2011-02-15 | Jernberg Gary R | Mixer with a catalytic surface |
| CA2623407A1 (fr) | 2008-02-28 | 2009-08-28 | Hydro-Quebec | Materiau d'electrode composite |
| EP2140933A1 (fr) * | 2008-07-02 | 2010-01-06 | Werner Soyez | Support de catalyseur structuré pour réacteurs tubulaires |
| US8278363B2 (en) * | 2009-03-23 | 2012-10-02 | Thomas Charles Holcombe | Fischer-tropsch reactions using heat transfer tubes with a catalyst layer on the outside surfaces |
| CN101818075B (zh) * | 2010-04-29 | 2013-06-12 | 华南理工大学 | 一种降低催化重整装置再接触工艺能耗的方法 |
| DE102011107933A1 (de) * | 2011-07-19 | 2013-01-24 | Thyssenkrupp Uhde Gmbh | Prozessintensivierung von Dampfreformern durch Verwendung angepasster Katalysatoren |
| CN103011077B (zh) * | 2011-09-27 | 2016-04-06 | 中国科学院宁波材料技术与工程研究所 | 一种催化重整制氢方法与催化装置 |
| WO2013044444A1 (fr) * | 2011-09-27 | 2013-04-04 | 中国科学院宁波材料技术与工程研究所 | Procédé de production d'hydrogène par reformage catalytique et unité catalytique |
| US8545775B2 (en) | 2011-10-20 | 2013-10-01 | Kellogg Brown & Root Llc | Reforming exchanger system with intermediate shift conversion |
| US9101899B2 (en) | 2011-10-20 | 2015-08-11 | Kellogg Brown & Root Llc | Reforming exchanger with integrated shift conversion |
| EP2812278B1 (fr) * | 2012-02-06 | 2023-04-19 | Helbio Societé Anonyme Hydrogen and Energy Production Systems | Reformeur intégré à la chaleur à combustion catalytique pour production d'hydrogène |
| US9295960B2 (en) * | 2012-03-23 | 2016-03-29 | United Technologies Corporation | Catalytic reaction in confined flow channel |
| RU2554008C1 (ru) | 2014-01-13 | 2015-06-20 | Общество с ограниченной ответственностью "Газохим Техно" | Реактор для парциального окисления углеводородных газов |
| WO2016049326A1 (fr) | 2014-09-24 | 2016-03-31 | Intellergy, Inc. | Appareil de reformage de déchets compact et pouvant être entretenu |
| ITUB20150576A1 (it) * | 2015-04-24 | 2016-10-24 | Hexsol Italy Srl | Scambiatore di calore a fascio tubiero e struttura perfezionata |
| ES2985615T3 (es) * | 2016-02-08 | 2024-11-06 | Kt Kinetics Tech S P A | Reactor endotérmico de eficiencia mejorada para la producción de gas de síntesis con recuperación de calor flexible para satisfacer la baja generación de vapor de exportación |
| EP3900820A1 (fr) * | 2020-09-21 | 2021-10-27 | Haldor Topsøe A/S | Échangeur de chaleur combiné a doubles tubes et réacteur de reformage à la vapeur comprenant deux types de lits catalytiques |
| JP2024505162A (ja) * | 2021-01-28 | 2024-02-05 | トプソー・アクチエゼルスカベット | 螺旋流の触媒熱交換反応器 |
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| DE1542473A1 (de) | 1966-08-10 | 1970-03-26 | Schmidt Dipl Phys Herbert | Verfahren und Vorrichtung fuer katalytische,chemische und physikalische Reaktionen in den Phasen gasfoermig,fluessig,gasfoermig-fluessig,gasfoermig-fest,fluessig-fest und fest |
| US3864083A (en) * | 1970-06-26 | 1975-02-04 | Exxon Research Engineering Co | Carbon Detection |
| CA1008667A (en) * | 1972-06-30 | 1977-04-19 | Foster Wheeler Corporation | Catalytic steam reforming |
| JPS52112607A (en) * | 1976-03-09 | 1977-09-21 | Agency Of Ind Science & Technol | Reformers |
| DE3068525D1 (en) * | 1979-09-06 | 1984-08-16 | Ici Plc | A process and apparatus for catalytically reacting steam with a hydrocarbon in endothermic conditions |
| US4363787A (en) * | 1979-12-18 | 1982-12-14 | Conoco Inc. | Monolith heat exchange reactor |
| JPS5817841A (ja) * | 1981-07-24 | 1983-02-02 | Mitsubishi Heavy Ind Ltd | 排ガス処理用触媒短繊維担体 |
| US4822521A (en) * | 1983-06-09 | 1989-04-18 | Uop | Integrated process and apparatus for the primary and secondary catalytic steam reforming of hydrocarbons |
| DE3532413A1 (de) * | 1985-09-11 | 1987-03-12 | Uhde Gmbh | Vorrichtung zur erzeugung von synthesegas |
| EP0260826B1 (fr) * | 1986-09-10 | 1990-10-03 | Imperial Chemical Industries Plc | Catalyseurs |
| US5011625A (en) * | 1989-12-11 | 1991-04-30 | The M. W. Kellogg Company | Autothermal steam reforming process |
| US6153152A (en) * | 1990-04-03 | 2000-11-28 | The Standard Oil Company | Endothermic reaction apparatus and method |
| US5362454A (en) * | 1993-06-28 | 1994-11-08 | The M. W. Kellogg Company | High temperature heat exchanger |
| CO4370053A1 (es) * | 1993-11-29 | 1996-10-07 | Shell Int Research | Proceso para la oxidacion parcial catalitica de hidrocarbu- ros |
| TW299345B (fr) * | 1994-02-18 | 1997-03-01 | Westinghouse Electric Corp | |
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| US5718881A (en) * | 1996-06-24 | 1998-02-17 | International Fuel Cells, Inc. | Catalytic reactor designed to reduce catalyst slumping and crushing |
| US5897282A (en) * | 1996-10-01 | 1999-04-27 | Comardo; Mathis P. | Catalytic reactor charging system and method for operation thereof |
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| EP0936182A3 (fr) * | 1998-02-13 | 2000-02-23 | Haldor Topsoe A/S | Méthode pour la mise en route sans suie des réacteurs de reformage autothermiques |
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| AU3978501A (en) * | 2000-02-18 | 2001-08-27 | Conoco Inc. | Reticulated ceramic foam catalysts for synthesis gas production |
| CA2411854A1 (fr) * | 2000-06-13 | 2001-12-20 | Robert A. Oswald | Catalyseurs supportes d'oxyde de nickel-magnesium et procedes de production de gaz synthetique |
| US6855272B2 (en) * | 2001-07-18 | 2005-02-15 | Kellogg Brown & Root, Inc. | Low pressure drop reforming exchanger |
| US7635456B2 (en) * | 2006-08-08 | 2009-12-22 | Kellogg Brown & Root Llc | Low pressure drop reforming reactor |
-
2001
- 2001-07-18 US US09/908,307 patent/US6855272B2/en not_active Expired - Lifetime
-
2002
- 2002-06-06 CA CA2389638A patent/CA2389638C/fr not_active Expired - Lifetime
- 2002-07-02 AT AT02014634T patent/ATE341525T1/de not_active IP Right Cessation
- 2002-07-02 ES ES02014634T patent/ES2269566T3/es not_active Expired - Lifetime
- 2002-07-02 EP EP02014634A patent/EP1277698B1/fr not_active Expired - Lifetime
- 2002-07-02 DE DE60215080T patent/DE60215080T2/de not_active Expired - Lifetime
- 2002-07-12 KR KR1020020040685A patent/KR100695052B1/ko not_active Expired - Lifetime
- 2002-07-17 MX MXPA02006987A patent/MXPA02006987A/es active IP Right Grant
- 2002-07-17 NO NO20023422A patent/NO20023422L/no not_active Application Discontinuation
- 2002-07-18 CN CNB021263035A patent/CN100448949C/zh not_active Expired - Lifetime
-
2005
- 2005-01-05 US US10/905,460 patent/US8216531B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| US8216531B2 (en) | 2012-07-10 |
| US6855272B2 (en) | 2005-02-15 |
| US20050086864A1 (en) | 2005-04-28 |
| DE60215080D1 (de) | 2006-11-16 |
| EP1277698A2 (fr) | 2003-01-22 |
| ATE341525T1 (de) | 2006-10-15 |
| KR20030009151A (ko) | 2003-01-29 |
| MXPA02006987A (es) | 2003-02-24 |
| US20030064011A1 (en) | 2003-04-03 |
| CN1397629A (zh) | 2003-02-19 |
| EP1277698B1 (fr) | 2006-10-04 |
| CA2389638A1 (fr) | 2003-01-18 |
| DE60215080T2 (de) | 2007-02-22 |
| CN100448949C (zh) | 2009-01-07 |
| NO20023422D0 (no) | 2002-07-17 |
| KR100695052B1 (ko) | 2007-03-14 |
| EP1277698A3 (fr) | 2004-03-24 |
| NO20023422L (no) | 2003-01-20 |
| ES2269566T3 (es) | 2007-04-01 |
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